CN206184438U - Liquid -phase hydrogenated reactor - Google Patents
Liquid -phase hydrogenated reactor Download PDFInfo
- Publication number
- CN206184438U CN206184438U CN201621233379.1U CN201621233379U CN206184438U CN 206184438 U CN206184438 U CN 206184438U CN 201621233379 U CN201621233379 U CN 201621233379U CN 206184438 U CN206184438 U CN 206184438U
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- CN
- China
- Prior art keywords
- cylinder
- liquid phase
- hydrogenation reactor
- motor
- phase hydrogenation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model discloses a liquid -phase hydrogenated reactor, including the barrel, be equipped with the motor directly over the barrel, the (mixing) shaft is connected to the motor, is equipped with stirring vane on the (mixing) shaft, and the motor both sides are equipped with manhole and hydrogenation hole, set up the baffle in the barrel, and the baffle below is equipped with the heat exchange tube that spirals and appear, and stirring vane's height is the same with heat exchange tube lower extreme height, and both ends are equipped with steam inlet respectively and are equipped with feed inlet, discharge gate, catalyst inlet with condensation export, barrel side about the heat exchange tube, are equipped with the emptying mouth below the barrel, the emptying mouth outside is equipped with the shrouding, liquid -phase hydrogenated reactor, structure science, the heat exchange tube setting is used with the agitator cooperation at the middle part, the heat exchange distribution of temperature is even, has improved feed stock conversion and product quality.
Description
Technical field
The utility model belongs to technical field of chemical, and in particular to a kind of liquid phase hydrogenation reactor.
Background technology
Hydrogenation reactor is one of important equipment of chemical industry, has two during current hydrogenation reactor use and lacks
Fall into：1st, complex structure, has that operational reliability is undesirable, service life is short, the low defect of reaction efficiency, and 2, use heat conduction originally
Oil is entered by hydrogenation reactor top, is exchanged heat with the paired stream of material shape for rising, in as heat exchange medium, conduction oil
Substantial amounts of reaction heat is taken away in portion's outflow；Can not be completely filled with for reactor due to conduction oil by this technique, cause top and the bottom temperature
Degree skewness, it is impossible to play optimal catalytic action, if temperature is less than reaction temperature, catalyst loses catalytic action, causes
Raw material availability declines, and reduces product quality, it is necessary to further be improved.
The content of the invention
To solve the above problems, the utility model discloses a kind of liquid phase hydrogenation reactor, scientific structure, temperature during heat exchange
Degree is evenly distributed, and improves feed stock conversion and product quality.
To reach above-mentioned purpose, the technical solution of the utility model is as follows：
A kind of liquid phase hydrogenation reactor, it is characterised in that：Including cylinder, motor is provided with directly over cylinder, the motor connects
Agitating shaft is connect, agitating shaft is provided with stirring vane, and motor both sides are provided with manhole and hydrogenation hole, dividing plate are set in cylinder, under dividing plate
Side is provided with the heat exchanger tube of spirally, and the height of stirring vane is highly identical with heat exchanger tube lower end, and heat exchanger tube upper and lower ends set respectively
There are steam inlet and condensate outlet, cylinder side is provided with charging aperture, discharging opening, catalyst inlet, and cylinder lower section is provided with discharging hole,
The discharging hole outside is provided with shrouding.
Used as a kind of improvement of the present utility model, the motor side is provided with exhaust outlet.
Used as a kind of improvement of the present utility model, the hydrogenation hole is provided with flowmeter.
Used as a kind of improvement of the present utility model, the cylinder inboard wall is provided with anticorrosive coat.
Used as a kind of improvement of the present utility model, the discharging hole side is provided with band thermocouple thermometer.
Used as a kind of improvement of the present utility model, the discharging hole side is provided with sample tap.
Used as a kind of improvement of the present utility model, the cylinder outside is provided with hanger.
The beneficial effects of the utility model are：
A kind of liquid phase hydrogenation reactor described in the utility model, scientific structure, heat exchanger tube is arranged on middle part, with agitator
Use cooperatively, heat exchange temperature is evenly distributed, improve feed stock conversion and product quality.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Reference numerals list：
1st, cylinder, 2, motor, 3, agitating shaft, 4, stirring vane, 5, manhole, 6, hydrogenation hole, 7, dividing plate, 8, heat exchanger tube, 9,
Steam inlet, 10, condensate outlet, 11, charging aperture, 12, discharging opening, 13, catalyst inlet, 14, discharging hole, 15, shrouding, 16,
Exhaust outlet, 17, flowmeter, 18, band thermocouple thermometer, 19, sample tap, 20, hanger.
Specific embodiment
With reference to the accompanying drawings and detailed description, the utility model is further elucidated, it should be understood that following specific embodiment parties
Formula is merely to illustrate the utility model rather than limits scope of the present utility model.It should be noted that making in description below
Word "front", "rear", "left", "right", "up" and "down" refer to the direction in accompanying drawing, and word " interior " and " outward " refer to respectively
Be directed towards or away from the direction of particular elements geometric center.
As illustrated, a kind of liquid phase hydrogenation reactor described in the utility model, including cylinder 1, it is provided with directly over cylinder 1
Motor 2, the connection agitating shaft 3 of the motor 2, agitating shaft 3 is provided with stirring vane 4, and the both sides of motor 2 are provided with manhole 5 with hydrogenation hole
6, dividing plate 7 is set in cylinder 1, the lower section of dividing plate 7 is provided with the heat exchanger tube 8 of spirally, height and the lower end of heat exchanger tube 8 of stirring vane 4
Highly identical, the upper and lower ends of heat exchanger tube 8 are respectively equipped with steam inlet 9 and condensate outlet 10, the side of cylinder 1 be provided with charging aperture 11,
Discharging opening 12, catalyst inlet 13, cylinder lower section are provided with discharging hole 14, and the outside of the discharging hole 14 is provided with shrouding 15.
A kind of liquid phase hydrogenation reactor described in the utility model, scientific structure is easy to use, during heat exchanger tube is arranged on
Portion, uses cooperatively with agitator, and heat exchange temperature is evenly distributed, and improves feed stock conversion and product quality.
The side of motor described in the utility model 2 is provided with exhaust outlet 16.
Hydrogenation hole 6 described in the utility model is provided with flowmeter 17.
The inwall of cylinder described in the utility model 1 is provided with anticorrosive coat, corrosion-resistant, increases the service life.
The side of discharging hole described in the utility model 14 is provided with band thermocouple thermometer 18.
The side of discharging hole described in the utility model 14 is provided with sample tap 19.
The outside of cylinder described in the utility model 1 is provided with hanger 20.
Technological means disclosed in the utility model scheme is not limited only to the technological means disclosed in above-mentioned implementation method, also
Including being combined constituted technical scheme by above technical characteristic.
Claims (7)
1. a kind of liquid phase hydrogenation reactor, it is characterised in that：Including cylinder, motor, the motor connection are provided with directly over cylinder
Agitating shaft, agitating shaft is provided with stirring vane, and motor both sides are provided with manhole and hydrogenation hole, and dividing plate, dividing plate lower section are set in cylinder
The heat exchanger tube of spirally is provided with, the height of stirring vane is highly identical with heat exchanger tube lower end, and heat exchanger tube upper and lower ends are respectively equipped with
Steam inlet and condensate outlet, cylinder side are provided with charging aperture, discharging opening, catalyst inlet, and cylinder lower section is provided with discharging hole, institute
State discharging hole outside and be provided with shrouding.
2. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The motor side is provided with exhaust
Mouthful.
3. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The hydrogenation hole is provided with flow
Table.
4. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The cylinder inboard wall is provided with anti-corrosion
Layer.
5. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The discharging hole side is provided with band heat
Dipole thermometer.
6. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The discharging hole side is provided with sampling
Mouthful.
7. a kind of liquid phase hydrogenation reactor according to claim 1, it is characterised in that：The cylinder outside is provided with hanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233379.1U CN206184438U (en) | 2016-11-17 | 2016-11-17 | Liquid -phase hydrogenated reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233379.1U CN206184438U (en) | 2016-11-17 | 2016-11-17 | Liquid -phase hydrogenated reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206184438U true CN206184438U (en) | 2017-05-24 |
Family
ID=58725800
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621233379.1U Expired - Fee Related CN206184438U (en) | 2016-11-17 | 2016-11-17 | Liquid -phase hydrogenated reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206184438U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998079A (en) * | 2018-09-03 | 2018-12-14 | 汤美侠 | A kind of extraction process of light oil |
| CN108998081A (en) * | 2018-09-18 | 2018-12-14 | 汤美侠 | A kind of diesel refining efficiency optimization method |
| CN109126667A (en) * | 2018-09-03 | 2019-01-04 | 汤美侠 | A kind of hydrogenator |
| CN110935413A (en) * | 2019-12-11 | 2020-03-31 | 西安交通大学 | Acid leaching tank device for red mud acid leaching process and red mud acid leaching process method |
| CN114471411A (en) * | 2022-02-11 | 2022-05-13 | 成都灿菱科技有限公司 | Reation kettle is used in chemical product processing of high temperature accuse precision |
-
2016
- 2016-11-17 CN CN201621233379.1U patent/CN206184438U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998079A (en) * | 2018-09-03 | 2018-12-14 | 汤美侠 | A kind of extraction process of light oil |
| CN109126667A (en) * | 2018-09-03 | 2019-01-04 | 汤美侠 | A kind of hydrogenator |
| CN108998081A (en) * | 2018-09-18 | 2018-12-14 | 汤美侠 | A kind of diesel refining efficiency optimization method |
| CN108998081B (en) * | 2018-09-18 | 2020-12-04 | 临沂文衡信息技术有限公司 | Diesel refining efficiency optimization method |
| CN110935413A (en) * | 2019-12-11 | 2020-03-31 | 西安交通大学 | Acid leaching tank device for red mud acid leaching process and red mud acid leaching process method |
| CN114471411A (en) * | 2022-02-11 | 2022-05-13 | 成都灿菱科技有限公司 | Reation kettle is used in chemical product processing of high temperature accuse precision |
| CN114471411B (en) * | 2022-02-11 | 2023-12-22 | 九江前发精细化工有限公司 | Reaction kettle for processing chemical products with high temperature control precision |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 Termination date: 20191117 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |